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14122 total products found.
Picture for 00046 SURFACE CHEMICAL AND MORPHOLOGICAL CHANGES
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00046 SURFACE CHEMICAL AND MORPHOLOGICAL CHANGES IN CORROSION PRODUCT LAYERS AND INHIBITORS IN COs CORROSION IN MULTIPHASE FLOWLINES

Product Number: 51300-00046-SG
ISBN: 00046 2000 CP
Author: S. Seal, K. Sapre and V. Desai, M. Gopal and W. P. Jepson
$20.00
Picture for Investigation of Microbial Sources in Corrosion of Crude Pipelines and Processing Facilities
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Investigation of Microbial Sources in Corrosion of Crude Pipelines and Processing Facilities

Product Number: MECC23-19973-SG
Author: Xiangyang Zhu; Abdullah H. Wadei; Husam S. Khanfar
Publication Date: 2023
$20.00

Many microorganisms occurring naturally in waters and soils can cause microbiologically influenced corrosion (MIC) on metal structures. Such microorganisms include sulfate-reducing bacteria (SRB), sulfate-reducing archaea (SRA), acid-producing bacteria (APB), methanogens, metal-oxidizing bacteria, metal-reducing bacteria, and nitrate-reducing bacteria. The activities of individual microbial species or a synergistic group of microbes alter the electrochemical processes on metal surface and produce a broad range of outcomes, such as pitting, crevice corrosion, under-deposit corrosion, and selective dealloying, in addition to an enhanced galvanic and erosion corrosion.
Corrosion Of UNS S31603 Under Partial Upgrading Of Bitumen Using Thermal Cracking
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Corrosion Of UNS S31603 Under Partial Upgrading Of Bitumen Using Thermal Cracking

Product Number: 51322-18059-SG
Author: Xue Han, Kaiyang Li, Yimin Zeng
Publication Date: 2022
$20.00

With the rapid economic development and the dramatic population growth, the demand on clean energy is continuously increasing.1 Due to the depletion of conventional crude oil reserves, the unconventional oil resources such as oil sands become more attractive.2 Canada has a total estimated oil sands reserves of 161.4 billion barrels by the end of 2020, accounting for 9.3% of the global reserves.3 The bitumen in the oil sands is extracted and transported through pipelines to the refineries with refining capabilities in Canada and the United States where the raw bitumen is processed to produce marketable synthetic crude oil (SCO). The proposed TransCanada system planned to connect the Alberta bituminous oil sands to the refineries as far as in Texas.4  
Picture for Real-Time Measurement of Aerospace Organic Coating Condition and Performance in Atmospheric Corrosion Conditions
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Real-Time Measurement of Aerospace Organic Coating Condition and Performance in Atmospheric Corrosion Conditions

Product Number: 51324-20742-SG
Author: Victoria Avance; Rebecca Marshall; Fritz Friedersdorf; Matthew Repasky; Henry Yuchi
Publication Date: 2024
$40.00
The purpose of this work is to develop a predictive coating condition model that processes continuous coating condition measurements to characterize changes in coating protection in atmospheric laboratory and outdoor environments. Zero resistance ammeter measurements across an interdigitated electrode composed of two different aerospace materials were used to monitor the inhibitive ability of a scribed coating and detect loss of inhibitor protection. Results will be presented that demonstrate the ability of a stochastic model to detect loss of inhibitor protection and predict coating failure in comparison to observational results. A description of the samples, electrochemical measurements, and test environments will be reported along with the approach used to extract parameters to model and predict coating performance.
Picture for Failure of Light Naphtha Discharge Pump in a 2-Stage Overhead System of Condensate Splitting Unit
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51318-10871-Failure of Light Naphtha Discharge Pump in a 2-Stage Overhead System of Condensate Splitting Unit

Product Number: 51318-10871-SG
Author: Gyutae Park / Jinseok Seo / Majid Abbasi / Yunjo Ro
Publication Date: 2018
$20.00

Recently, a light naphtha discharge pump (made of UNS J91150 casing and impeller) malfunctioned, which caused severe damage to the impeller. Details of the failure analysis will be presented and discussed.
Picture for Flame Retardant Polyurethane Corrosion Protective Coating
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Flame Retardant Polyurethane Corrosion Protective Coating

Product Number: 51322-17696-SG
Author: Mohammad Mizanur Rahman
Publication Date: 2022
$20.00

Metal and its structures corrosion is a natural process. The process started and accelerated in the presence of electrolytes [1, 2]. Thus, it's highly encouraged to stop this electrolyte passage. One of the ways to resist the passage of electrolytes is by making a barrier. The most popular method of such a barrier is an organic coating which mainly comes from polymer resin along with pigments, and additives. Different organic coatings are being used to make a barrier that can ultimately protect the metals and their structures. Epoxy, polyurethane (PU), and acrylate coatings are widely being used for this purpose.
Picture for 06312 Application of Pulsed Eddy Current Corrosion
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06312 Application of Pulsed Eddy Current Corrosion Monitoring in Refineries and Oil Production Facilities

Product Number: 51300-06312-SG
ISBN: 06312 2006 CP
Author: Paul C.N. Crouzen, Ian J. Munns, W. Verstijnen, Roy C. Hulsey
$20.00
Picture for Corrosion Protection Status And Countermeasures Of Shield Tunnel Pipeline
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Corrosion Protection Status And Countermeasures Of Shield Tunnel Pipeline

Product Number: 51322-17518-SG
Author: Su Jin
Publication Date: 2022
$20.00

At present, there were ten common crossing modes in long-distance oil and gas pipelines[1,2]. There were six ways of tunneling, such as large excavation, horizontal directional drilling, shield tunnel, drilling and blasting tunnel, ramming pipe and pipe jacking. There were four ways of spanning methods, such as truss crossing, arch bridge crossing, suspension cable crossing and cable-stayed bridge crossing. Crossing by shield tunneling, as a pipeline laying method with high mechanization and automation, extensive applicable strata and high safety, has been widely used in recent years.
Picture for Corrosion evaluation of tubing steels and material selection in the CO2/H2S coexistent environme
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51318-11477-Corrosion evaluation of tubing steels and material selection in the CO2/H2S coexistent environment

Product Number: 51318-11477-SG
Author: Nai-yan ZHANG / Zhi ZHANG / Wen-tao ZHAO / Lian LIU / Taihe SHI
Publication Date: 2018
$20.00

To evaluate the applicability of the tubing steels, the corrosion behavior and stress corrosion cracking of tubing steels (P110S, P110-13Cr and duplex stainless steel 2205) were investigated under different H2S partial pressures and temperature.
Picture for Corrosion of Steel in Concrete: Prevention, Diagnosis, Repair-2nd Ed

Corrosion of Steel in Concrete: Prevention, Diagnosis, and Repair, 2nd edition

Product Number: 38604
ISBN: 9783527331468
Author: Luca Bertolini, by Bernhard Elsener, Pietro Pedeferri, Elena Redaelli, Rob B. Polder
Publication Date: 2014
$190.00

 

Corrosion of steel in concrete.  Mechanisms. Practical consequences. Carbonation and chlorides. Hydrogen embrittlement. Diagnosis. Monitoring. Repair. European standards. Design and maintenance of concrete structures.  Knowledge, tools, and methods.  2nd edition 2014 Wiley
Picture for Methods of Monitoring Reinforced Concrete Corrosion in Formulations for Nuclear Facilities
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Methods of Monitoring Reinforced Concrete Corrosion in Formulations for Nuclear Facilities

Product Number: 51317--9154-SG
ISBN: 9154 2017 CP
Author: Damián Vazquez
Publication Date: 2017
$20.00

Two concrete formulations, one of ordinary portland cement and one of pozzolanic portland cement, are compared by rebar corrosion criteria. Both formulations are candidates for nuclear applications whose durability requirement is higher than 300 years.
Picture for Cathodic Protection Of Mooring Chain In Offshore Environment
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Cathodic Protection Of Mooring Chain In Offshore Environment

Product Number: 51322-17722-SG
Author: Faisal Shahzad, Nils Olav Digre, Kristian Varne
Publication Date: 2022
$20.00

Corrosion in Mooring systems for permanently moored floating production units has been identified as a problem area by authorities as well as industry. A Joint Industry Project (JIP) initiated by the Bureau of Safety and Environmental Enforcement (BSEE) with participation from major global oil and gas operators as well as equipment suppliers was established in 2014 to review the problem area. 1 Studies performed as a part of this program have shown that especially mooring chains located in tropical waters have shown signs of rapid corrosion, both general and localized with corrosion rates significantly larger than those specified in design standards. Increased corrosion allowance, as well as increased inspection requirements, have been recommended and corrosion has been reported as the leading cause for pre-emptive replacement of mooring.
Picture for NACE Publication 01110-2019, Stray-Current-Induced Corrosion in Reinforced and Prestressed Concrete Structures
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NACE Publication 01110-2019, Stray-Current-Induced Corrosion in Reinforced and Prestressed Concrete Structures

Product Number: 24241-2019
Publication Date: 2019
$109.00

The corrosion of reinforcing and prestressing steel in concrete structures caused by stray currents.  The history of stray-current corrosion, sources, mechanisms, effects on structures, detection and mitigation. 
Ultra-Low VOC Waterborne Alkyd Coatings with Exceptional Corrosion Resistance
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Ultra-Low VOC Waterborne Alkyd Coatings with Exceptional Corrosion Resistance

Product Number: 51216-018-SG
Author: Erin Vogel, Bob Bills, Marty Beebe, Christina Ellison, Jamie Sullivan, Vennesa Williams
Publication Date: 2016
$20.00

Solventborne alkyd resins are widely used in industrial coatings because of their excellent gloss, good adhesion and wetting properties as well as excellent compatibility with other resin types. In many regions, however, the consumption of alkyds is diminishing as stringent environmental regulations drive the coatings industry towards lower volatile organic compound (VOC) systems. Waterborne (WB) coating systems have replaced some solventborne (SB) alkyd paints; however, these WB coatings typically do not offer the same performance as their solventborne counterparts. 
Picture for Corrosion Properties of UNS S83071 in Acid and Caustic Environments
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Corrosion Properties of UNS S83071 in Acid and Caustic Environments

Product Number: 51324-21103-SG
Author: Oscar Öhlin; Daniel Gullberg
Publication Date: 2024
$40.00
UNS S83071 is a recently developed super duplex stainless steel with the composition 30Cr-7Ni-3.5Mo-N, optimized for general corrosion resistance. Previously presented data have shown that UNS S83071 has excellent acid corrosion resistance as well as excellent resistance to pitting and crevice corrosion. Furthermore, the grade has very high mechanical strength with good microstructure stability and weldability. This paper presents new data from general corrosion testing of UNS S83071 in various acid and caustic environments, including formic acid, nitric acid, phosphoric acid, sodium hydroxide, and others. The results show that UNS S83071 has excellent acid and caustic general corrosion resistance, demonstrating the suitability of the grade in several corrosive environments. UNS S83071 is a good candidate material for applications within chemical industry, and the presented data can assist in material selection e.g. for heat exchangers or equipment used in acid or caustic production plants.
Picture for 51318-11180- A Corrosion Inhibition Study of Carbon Steel in a 0.7 MWe Pilot CO2 Capture Process
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51318-11180- A Corrosion Inhibition Study of Carbon Steel in a 0.7 MWe Pilot CO2 Capture Process

Product Number: 51318-11180-SG
Author: Wei Li / James Landon / Bradley Irvin / Jesse Thompson / Heather Nikolic / Kunlei Liu
Publication Date: 2018
$20.00

Corrosion behavior of carbon steel in an in-house solvent was investigated in a pilot-scale post combustion CO2 capture process. Carbon steel specimens were placed where corrosion problems were previously found in the stripper column and the CO2-rich amine piping.
Picture for 97325 MODELLING HUMAN INTERVENTIONS IN
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97325 MODELLING HUMAN INTERVENTIONS IN CORROSION FAILURES

Product Number: 51300-97325-SG
ISBN: 97325 1997 CP
Author: K R Trethewey, P.R Roberge
$20.00
Picture for 03235 ATMOSPHERIC CORROSION SUPPRESSION THROUGH
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03235 ATMOSPHERIC CORROSION SUPPRESSION THROUGH CONTROLLED HUMIDITY PROTECTION (CHP), AN OPERATIONAL READINESS AND FORCE MULTIPLIER

Product Number: 51300-03235-SG
ISBN: 03235 2003 CP
Author: James H. Martin
Publication Date: 2003
$20.00

Presents: Relationship between humidity and degradation rates. CHP systems deployment throughout the Department of Defense. CHP systems in use on Aircraft, etc. DoD, U.S. Marine Corps and Naval Aviation CHP policy. Independent CHP performance / economic analyses by GAO. User-reported performance
Picture for Diagnosis of Internal Corrosion in Pipelines Based on Mapping Adverse Operational Conditions
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Diagnosis of Internal Corrosion in Pipelines Based on Mapping Adverse Operational Conditions

Product Number: 51319-13250-SG
Author: Yuri Fairuzov, Victor Fairuzov
Publication Date: 2019
$20.00

Upstream oil and gas companies operate oil gathering systems comprising a flowline network and process facilities that transport the flow of produced fluids from the wells to a main processing plant. The frequency of corrosion related leaks has increased recently despite a corrosion inhibitor is injected at the wellhead into all flowlines. A root-cause analysis conducted by several companies revealed that severe internal corrosion was caused by a low fluid flow velocity an increasing water cut and the presence of sulfate-reducing bacteria (SRB) in the production streams. Nevertheless it was not clear why some of the flowlines may leak while others do not leak despite the composition of produced fluids principal design parameters (diameter and length) dosage of corrosion inhibitor and environmental conditions of the flowlines are similar. A diagnostic analysis of different oil flowlines of was carried out to gain an understanding of why a first group of oil flowlines is developing leaks and why a second group of flowlines has not experienced leaks. The methodology used for the diagnostic analysis comprises 1) Ultra-High Definition simulation of 3-phase or 4-phase flow of gas oil water and solids; 2) 3D imaging of phase distributions inside critical sections of the oil flowlines as per NACE ICDA; 3) mapping adverse operational conditions; and 4) the determination of probability of failure in the critical sections based on criteria depending on the severity of operating conditions inside and outside the flowlines. It was found that multiple sections were exposed to stagnant water and/or had a fraction of internal surface area covered by a stationary bed of solids (formation solids produced from the well). The identified causes of potential leaks comprise the following failure mechanisms: a) metal loss caused by colonies of SRB b) composed load acting on the pipe wall and c) cyclic" thermal expansion/contraction of the flowlines due to seasonal ambient temperature variations. One of the surprising findings of this study was that a shorter flowline with a lower water cut may have multiple leaks while a longer flowline with a higher water may not leak at all approximately for the same period after commissioning. This result was explained with help of maps of adverse operational conditions constructed for the two groups of flowlines. Immediate corrective mitigation actions and preventive actions were implemented to reduce leak frequency including the installation of a novel automatic flushing system.
Picture for A Study on Preferential Weld Metal Corrosion in 316 Austenitic Stainless Steel in HCl Containing Environments
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A Study on Preferential Weld Metal Corrosion in 316 Austenitic Stainless Steel in HCl Containing Environments

Product Number: 51319-13248-SG
Author: Hyunjoon Park
Publication Date: 2019
$20.00

Type 316 austenitic stainless steel is routinely used to handle dry hydrogen chloride gases in petrochemical processes. However the presence of moisture changes the corrosion behavior by the formation of liquid hydrochloric acid. When 316 welds are exposed to HCl environment it is often found that weldments undergo severe corrosion compared to the base material. In order to clarify the mechanism of preferential weld corrosion microstructural analysis including determination of phase composition of 316 welds which had experienced preferential corrosion in condensed HCl was performed using SEM TEM and EBSD. In addition laboratory immersion test was also conducted to understand the corrosion behavior in aerated HCl solution. Corrosion arrack preferentially occurred either at austenite in dendrite cores or ferrite in inter-and intra-dendritic boundary depending on the concentration of HCl. It is suggested that ferrite is more resistant to mild HCl corrosion than austenite due to the stability of passive film. On the other hand in highly reducing HCl solutions ferrite has inferior corrosion resistance compare to austenite. Galvanic corrosion between the two constituent phases is proposed to lead to selective weld metal corrosion.
Picture for 96221 CORROSION INHIBITORS IN HYDROCARBON
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96221 CORROSION INHIBITORS IN HYDROCARBON SYSTEMS

Product Number: 51300-96221-SG
ISBN: 96221 1996 CP
Author: A.Jayaraman, R.C.Saxena
$20.00
Picture for 96657 COMPUTER LEARNING SYSTEMS IN CORROSION
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96657 COMPUTER LEARNING SYSTEMS IN CORROSION

Product Number: 51300-96657-SG
ISBN: 96657 1996 CP
Author: C.P. Sturrock, W.F. Bogaerts
$20.00
Picture for Assessing Corrosion Risk and Selection of Appropriate Testing Programs for Gas and Gas-Condensate Pi
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51317--9713-Assessing Corrosion Risk and Selection of Appropriate Testing Programs for Gas and Gas-Condensate Pipelines

Product Number: 51317--9713-SG
ISBN: 9713 2017 CP
Author: Caroline Simpson
Publication Date: 2017
$20.00

There is uncertainty about the best way to determine the corrosion risk for gas-condensate pipelines, and use of chemical inhibitors as mitigation strategy. We present considerations when devising corrosion mitigation and inhibition strategies, as well as a recommended test for inhibitor qualification.

 

 

 
Picture for Improvements in the Use of Indirect Inspection Tools and Data Interpretation
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51318-10657-Improvements in the Use of Indirect Inspection Tools and Data Interpretation

Product Number: 51318-10657-SG
Author: S.M. Segall / R.A. Gummow / D. Fingas / Cory Bradshaw
Publication Date: 2018
$20.00

Methods for dealing with sources of errors affecting the accuracy of the Direct Current Voltage Gradient (DCVG) coating defect identification and sizing tool.
Picture for Proposal of a New Corrosion Index for Domestic Tap Water In Japan
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Proposal of a New Corrosion Index for Domestic Tap Water In Japan

Product Number: 51323-19056-SG
Author: Yuji Nakamura, Yasuki Matsukawa, Shinji Okazaki, Shukuji Asakura
Publication Date: 2023
$20.00

Japanese tap water has a low calcium hardness compared with those of countries in Europe and the Americas. There are many steep mountains and volcanos in Japan. These geological factors lead to features such as short rivers with water rich in SiO2. This leads to a lack of calcium compounds in river water because the flow rate is high and the dissolution rate of CaCO3 into water is low.
The Futility and Folly of Seeking the Accelerated Corrosion Holy Grail
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The Futility and Folly of Seeking the Accelerated Corrosion Holy Grail

Product Number: 41215-885-SG
Author: Carl W. Reed, Kat Coronado
Publication Date: 2015
$20.00

Since the dawn of mankind, or at least since the advent of the very first accelerated corrosion cabinet, it has been the goal of coatings evaluators to develop an accelerated corrosion testing protocol which reflects the real world of corrosion in totality. There have been passionate arguments promoting one or another testing protocol while demonizing others, but that one protocol has yet to be developed to everyone’s satisfaction. 
Picture for Corrosion Behavior of Austenitic Stainless Steels and Nickel alloys in Simulated High Temperature Gethermal Environment
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51318-11058-Corrosion Behavior of Austenitic Stainless Steels and Nickel alloys in Simulated HT Geth. Environm.

Product Number: 51318-11058-SG
Author: Andri Isak Thorhallsson / Sigrun Nanna Karlsdottir / Andri Stefansson
Publication Date: 2018
$20.00

A 3-week corrosion testing of UNS N06625 was conducted in supercritical fluid at 350°C and 10 bars to simulate a geothermal environment where other alloys had been tested. Some localized corrosion occurred at a rate similar to previous results.
Picture for 08173 Cavitation and Erosion Damage of Reboiler Stripper Tubes in Gas Manufacturing Industry
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08173 Cavitation and Erosion Damage of Reboiler Stripper Tubes in Gas Manufacturing Industry

Product Number: 51300-08173-SG
ISBN: 08173 2008 CP
Author: Hussein Rahmatalla, Mohammed Maqbool Ahmed, and Abdulla Radi Al-Hajri
Publication Date: 2008
$20.00

Two successive leakages were reported in the heat exchanger composed of 8 rows of finned tubes of the convection section of the condensate stripper re-boiler.  A comprehensive study (Failure Analysis) has been conducted to reveal the form of failure. The failure was recognized as erosion and cavitation damage.
Picture for RP0390-Maintenance and Rehabilitation Considerations for Corrosion Control of Atmospherically Exposed Existing Steel-Reinforced Concrete Structures-HD2006
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RP0390-HD1998-SG Maintenance and Rehabilitation Considerations for Corrosion Control of Atmospherically Exposed Existing Steel-Reinforced Concrete Structures-HD2006

Product Number: 21044-HD1998
ISBN: 1-57590-059-9
Author: NACE International
Publication Date: 1998
$179.00

This standard presents corrosion control guidelines that are applicable to existing atmospherically exposed structures made of conventionally reinforced concrete. Historical Document 1998
Picture for 00005 PROTECTIVE PROPERTIES OF CRUDE OILS
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00005 PROTECTIVE PROPERTIES OF CRUDE OILS IN CO2 AND H2S CORROSION

Product Number: 51300-00005-SG
ISBN: 00005 2000 CP
Author: Marta Castillo, Hern~in Rincon, Simona Duplat, Jose Vera, Evaristo Baron
$20.00
Picture for Determination of the Corrosion Rate of Thermally Spayed Aluminum (TSA) in Simulated Marine Service
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Determination of the Corrosion Rate of Thermally Spayed Aluminum (TSA) in Simulated Marine Service

Product Number: 51320-14650-SG
Author: Shiladitya Paul, Dave Harvey
Publication Date: 2020
$20.00

Operators desire extended life of offshore facilities, structures and components to improve affordability, and to increase their availability in later years of operation. Whilst maintenance and replacement of topside facilities is possible, critical to this objective is the design and construction of supporting infrastructure and facilities capable of withstanding splash and tidal zone corrosion for the lifetime of the structure with minimum maintenance.  

Thermally sprayed aluminum (TSA) is increasingly applied in marine environments as a corrosion mitigation solution but few studies provide quantitative corrosion rate data, from which a lifetime of little or no maintenance can be predicted. A technology review was undertaken to establish current working practice and experience related to the mitigation of splash and tidal zone corrosion. A number of coating systems (thermally sprayed, organic paints and duplex combined thermal spray and paint), currently used in the splash and tidal zone of offshore structures, were identified. Thermal spray coatings with and without aluminum-silicone sealant were prepared and tested in alternate immersion using linear polarisation resistance (LPR) methods. The data were analysed and corrosion rates values were obtained. 
Picture for Inhibition of Pitting Corrosion in Simulated Liquid Radioactive Waste
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51317--9689-Inhibition of Pitting Corrosion in Simulated Liquid Radioactive Waste

Product Number: 51317--9689-SG
ISBN: 9689 2017 CP
Author: Bruce Wiersma
Publication Date: 2017
$20.00

The Hanford Site in Richland, WA stores liquid radioactive waste in underground, carbon steel tanks. Electrochemical corrosion testing was performed to determine new limits that optimize the chemistry control, yet are robust enough to inhibit against the possibility of increased concentrations of aggressive species.

 
Picture for 07198 Stainless Steel Pitting in Chloride-Sulfate Solutions - The Role of Cations
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07198 Stainless Steel Pitting in Chloride-Sulfate Solutions - The Role of Cations

Product Number: 51300-07198-SG
ISBN: 07198 2007 CP
Author: P. Pohjanne, L. Carpen, P. Kinnunen, J. Ramo, A. Sarpola, M. Riihimaki, and T. Hakkarainen
Publication Date: 2007
$20.00

 In this study the pitting behavior of stainless steel type AISI 304 (EN 1.4301) has been studied in various binary mixtures of MgSO4, K2SO4 or Li2SO4 with NaCl. Results are compared to those obtained in binary mixtures of Na2SO4 with NaCl as well as in plain NaCl.
Picture for High Temperature Corrosion Quantification in Renewable Diesel and Sustainable Aviation Fuel Applications
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High Temperature Corrosion Quantification in Renewable Diesel and Sustainable Aviation Fuel Applications

Product Number: MECC23-20056-SG
Author: Sridhar Srinivasan, Gerrit Buchheim
Publication Date: 2023
$20.00

The authors have developed and introduced a molecular mechanistic model that quantifies and predicts simultaneous naphthenic acid and sulfidation (SNAPS) corrosion rates. This was subsequently presented as a definitive mechanistic corrosion prediction framework describing the molecular basis of the model’s reactions, kinetics, and mass transport of reactive organic sulfur compounds (ROSC) to vessel walls . In this molecular model, sulfidation corrosion is calculated for direct heterolytic reaction of ROSC with solid surfaces. As recently reported, % total S and ppm mercaptans are used as input for the ROSC reactions in the model (Figure 1).
Picture for 11334 Green Shelters Dehumidification for Corrosion Attenuation & Improved Maintenance Flexibility
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11334 Green Shelters Dehumidification for Corrosion Attenuation & Improved Maintenance Flexibility

Product Number: 51300-11334-SG
ISBN: 11334 2011 CP
Author: Doug Banning
Publication Date: 2011
$20.00

Corrosion prevention and control for equipment is a costly and decreasingly effective activity for the Air Force, especially under scenarios to austere locations.  One concept for remedy is a modular shelter, powered with mobile generators using integrated energy sources to reduce operational costs. 
Picture for Prediction Of The Mitigated Corrosion For Inhibitor Applications In Oil And Gas Operations
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Prediction Of The Mitigated Corrosion For Inhibitor Applications In Oil And Gas Operations

Product Number: 51321-16704-SG
Author: J. Sonke; Y. Zheng; J. Moloney
Publication Date: 2021
$20.00
Picture for The Performance of Corrosion Resistant Ni-Cr-Mo Alloys in Concentrated Hydrochloric Acid
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51317--9639-The Performance of Corrosion Resistant Ni-Cr-Mo Alloys in Concentrated Hydrochloric Acid

Product Number: 51317--9639-SG
ISBN: 9639 2017 CP
Author: Suresh Divi
Publication Date: 2017
$20.00

This paper is to study the corrosion performance of various Ni based alloys in high concentrations of HCl acids below the boiling point. Nickel-based alloys C-276 (UNS N10276), C-22 (UNS N06022), C-2000 (UNS N06200), Hybrid-BC1 (UNS N10362) and B-3 (UNS N10675) were investigated.

 
Picture for 02274 EFFECTIVENESS OF CORROSION INHIBITORS...
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02274 EFFECTIVENESS OF CORROSION INHIBITORS IN RETARDING PROPAGATION OF LOCALISED CORROSION

Product Number: 51300-02274-SG
ISBN: 02274 2002 CP
Author: A. Turnbull, D. Coleman, A.J. Griffiths, P.E. Francis, and L. Orkney
Publication Date: 2002
$20.00

In many service applications excursions in solution chemistry, temporary loss of inhibitor, or transient increases in temperature may give rise to localised corrosion. To test the return of inhibition when the loss is remedied, the use of an artificial pit has been investigated using simulations of cooling water and of of oil production formation water.
Picture for Marine Structural Integrity Subject to Mechano-Electrochemical Induced Corrosion
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51317--9656-Marine Structural Integrity Subject to Mechano-Electrochemical Induced Corrosion

Product Number: 51317--9656-SG
ISBN: 9656 2017 CP
Author: Yikun Wang
Publication Date: 2017
$20.00

An experimental protocol including in situ potentiostat and quasi-static tensile tests to provide an improved understanding of the corrosion behavior of UNS G10210 steel. A local-global finite element method has been proposed to model a steel plate at a ship compartment scale under uniaxial quasi-static tensile/compressive loading.

 
Picture for Chemical Methods for Controlling Corrosion in Oil and Gas Activities
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Chemical Methods for Controlling Corrosion in Oil and Gas Activities (E-book)

Product Number: 37622-E
Author: Wayne Frenier
Publication Date: 2017
$105.00

Overview of the science and technology of corrosion control using chemicals. Some knowledge of corrosion and chemistry is assumed.  Chemical and mechanical principles. Corrosion inhibitors (CI).  Application methods. O&G environment. 2017 NACE

 
Picture for Effect on Corrosion Behavior of the Heat Treatment Temperature of 30408 Stainless Steel
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51317--9690-Effect on Corrosion Behavior of the Heat Treatment Temperature of 30408 Stainless Steel

Product Number: 51317--9690-SG
ISBN: 9690 2017 CP
Author: Bo Zhao
Publication Date: 2017
$20.00

Samples simulating the continuous changing structures of UNS S30400 heat affected zone (HAZ) were prepared for examination using metallographic structural analysis, corrosion morphological observations, and traditional electrochemical measurements to characterize the intergranular corrosion and pitting resistance.

 
Picture for Influence of Operating Temperature on the Corrosion of UNS S30400 Steel under Catalytic Hydrodeoxygenation of Pyrolysis Oil by Supercritical Ethanol with In-situ Hydrogen Source
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Influence of Operating Temperature on the Corrosion of UNS S30400 Steel under Catalytic Hydrodeoxygenation of Pyrolysis Oil by Supercritical Ethanol with In-situ Hydrogen Source

Product Number: 51323-19012-SG
Author: Mingyuan Zhang, Minkang Liu, Xue Han, Yimin Zeng, Chunbao Xu
Publication Date: 2023
$20.00

Bio-oils are renewable and clean energy sources, which can be used to partial or completely replace fossil fuel. Fast pyrolysis is a promising and by far the only industrially realized approach to convert dry biomass into biofuels, particularly the liquid bio-oils. However, the poor quality of fast pyrolysis oil including thermal instability, high viscosity and acidity, high oxygen and water content, and low heating value makes it hard to be directly used as transportation fuels.
Picture for Casing Corrosion in Geothermal Environments Containing Sulfuric Acid
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Casing Corrosion in Geothermal Environments Containing Sulfuric Acid

Product Number: 51324-20932-SG
Author: Joseph Thevakumar; Joshua Owen; Richard Barker; Evgeny Barmatov
Publication Date: 2024
$40.00
This work focusses on understanding corrosion severity and material performance within model geothermal sulfuric acid (H2SO4)-containing environments. With the use of a tantalum-lined high pressure/high temperature autoclave, the corrosion behavior of N80 carbon steel was compared against duplex stainless steel when exposed to H2SO4 solutions (pH 2-4) at temperatures up to 150°C. Electrochemical linear polarization resistance measurements were implemented to gather real time corrosion kinetic data. Complimentary ex-situ analyses (scanning electron microscopy and white light interferometry) were conducted to understand the corrosion mechanism and quantify localized corrosion rates. A quantitative relationship was identified in terms of pH, temperature and metal corrosion for the selected materials to highlight material capability within such low pH geothermal environments.
Picture for SP0106-2006, Control of Internal Corrosion in Steel Pipelines and Piping Systems
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SP0106-2018, Control of Internal Corrosion in Steel Pipelines and Piping Systems

Product Number: 21111-SG
ISBN: 1-57590-208-7
Publication Date: 2018
$109.00

This standard presents recommended practices for the control of internal corrosion in steel pipelines and piping systems used to gather, transport, or distribute crude oil, petroleum products, or gas. It is meant to serve as a guide for establishing minimum requirements for control of internal corrosion in crude oil gathering and flow lines, crude oil transmission, hydrocarbon products, gas gathering and flow lines, gas transmission, and gas distribution.
Picture for Comparison Of Atmospheric Corrosion Of Silver Across Multiple Locations
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Comparison Of Atmospheric Corrosion Of Silver Across Multiple Locations

Product Number: 51322-17621-SG
Author: Douglas C Hansen, Ronald Zeszut, David Rubino
Publication Date: 2022
$20.00

Atmospheric corrosion of bare metals is a constantly occurring process that can cause significant damage to metal components and structures. For this reason, it has been extensively studied, especially for steel and aluminum alloys.1-8 Environmental exposure testing is a common method for studying and characterizing the corrosion severity of a location, which allows for comparison with other regions. Much of this data collection is directed toward development of predictive models for corrosion processes, with the goal of estimating corrosion damage based on environmental conditions.
Picture for Sour Corrosion Products Formed in High H2S Gas Wells
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Sour Corrosion Products Formed in High H2S Gas Wells

Product Number: 51319-12866-SG
Author: Qiwei Wang
Publication Date: 2019
$20.00

Sour corrosion products could have a significant impact on the corrosion rate of carbon steel in H2S environments. It is widely believed that the different iron sulfides have different effects due to their distinct physico-chemical properties. Therefore an in-depth knowledge on the formation conditions of these polymorphous phases is of virtual importance for the understanding of sour corrosion process.Many studies have been performed to determine the key factors such as temperature solution pH H2S partial pressure and the duration of exposure in the formation of polymorphous iron sulfides; yet their formation conditions stability and phase relations are still not fully understood. This is partially due to the complex nature of sulfide and iron chemistry and their sensitiveness to oxygen. Seemingly minor changes in test conditions can often lead to dramatically different results.In this paper we present a statistic study on the corrosion products formed in some high temperature and high H2S gas wells in Saudi Arabia. Large numbers of deposits collected from downhole tubulars and wellhead manifolds are characterized for phase compositions. Results show a wide range of mineral phases and significant variation among the samples analyzed. The polymorphous iron sulfides include pyrrhotite pyrite marcasite troilite mackinawite and greigite in the order of abundance. Ferric iron compounds such as hematite magnetite akaganeite goethite and lepidocrocite are also identified in many samples. In addition ferrous iron products especially siderite are often detected. Based on the deposit structure analysis the formation mechanisms of these different types of corrosion products are discussed. It is hoped that the results from this work will contribute to further understanding of the sour corrosion process and provide value for corrosion and scale mitigation in oil and gas fields.
Picture for RP0170 - Protection of Austenitic Stainless Steel From Polythionic Acid Stress Corrosion Cracking During Shutdown of Refinery Equipment-HD1985
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RP0170-1985 - Protection of Austenitic Stainless Steel From Polythionic Acid Stress Corrosion Cracking During Shutdown of Refinery Equipment-HD1985

Product Number: 21002-HD1985
Author: NACE
Publication Date: 1983
$179.00

Methods to protect austenitic stainless steel from polythionic acid stress corrosion cracking (SCC) found to occur during downtimes and contiguous shutdown and start-up periods.  Historical Document 1986
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51315-5664-Nanometer Precision Ultrasonic Corrosion Monitoring

Product Number: 51315-5664-SG
ISBN: 5664 2015 CP
Author: Attila Gajdacsi
Publication Date: 2015
$20.00

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